CN103575077A - Multi-layer belt type drying system - Google Patents
Multi-layer belt type drying system Download PDFInfo
- Publication number
- CN103575077A CN103575077A CN201310548774.3A CN201310548774A CN103575077A CN 103575077 A CN103575077 A CN 103575077A CN 201310548774 A CN201310548774 A CN 201310548774A CN 103575077 A CN103575077 A CN 103575077A
- Authority
- CN
- China
- Prior art keywords
- drying
- air
- layer
- belt
- drying system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000001035 drying Methods 0.000 title claims abstract description 67
- 239000000463 material Substances 0.000 claims abstract description 35
- 238000001816 cooling Methods 0.000 claims abstract description 29
- 238000009826 distribution Methods 0.000 claims description 5
- 238000005192 partition Methods 0.000 claims description 3
- 239000000428 dust Substances 0.000 claims description 2
- 238000007791 dehumidification Methods 0.000 claims 1
- 230000005540 biological transmission Effects 0.000 abstract description 20
- 239000007789 gas Substances 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 239000002918 waste heat Substances 0.000 abstract description 5
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 10
- 239000003077 lignite Substances 0.000 description 8
- 239000003245 coal Substances 0.000 description 7
- 238000001704 evaporation Methods 0.000 description 6
- 238000007599 discharging Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000013467 fragmentation Methods 0.000 description 2
- 238000006062 fragmentation reaction Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000012271 agricultural production Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Images
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a multi-layer belt type drying system. The multi-layer belt type drying system comprises a drying box with an exhaust port in the top and multiple layers of transmission net belts in the drying box, wherein the input end of the lower-layer transmission net belt is connected with the output end of the adjacent upper-layer transmission net belt, and a plurality of circulation fans are arranged under each layer of transmission net belt. A horizontal separation plate dividing the drying box into a drying chamber and a cooling chamber is arranged in the drying box, an air feeding port is formed in the bottom of the cooling chamber, a draught fan used for exhausting the air is arranged inside the cooling chamber, the air feeding port and the draught fan are arranged at two sides of the transmission net belts, a heater is arranged in the drying chamber, an air inlet of the heater is communicated with an air outlet of the draught fan, and a plurality of air outlets corresponding to the transmission net belts in the drying chamber one to one are formed in the heater. The multi-layer belt type drying system is simple in structure and reasonable in arrangement, preheats a heating medium by recycling waste heat of off gas and utilizing dried upgrading materials with high temperature, and lowers the energy consumption in the drying process.
Description
Technical field
The present invention relates to a kind of belt drying system, be specifically related to a kind of Multi-layer belt type drying system.
Background technology
The lignite resource reserves that China has been found that are huge and cheap, however the brown coal minimum coal that is degrees of coalification, and porosity is large, volatile matter is high, oxygen content can reach 15%～30%, moisture is high, total moisture generally can reach 20～50%, and very easily weathering in air belongs to low, middle low calorific value coal, be unfavorable for that long-distance transport stores with long-time, because moisture is high, the direct combustion power generation of undried, flame temperature is low, after-flame difficulty, the thermal efficiency is low.At present, along with the development of industrial and agricultural production and the sharp increase of urban population, a large amount of sanitary sewages and industrial wastewater have been brought, make the output of mud increasing, the municipal sludge calorific value of undried is very low, when moisture content is 80%, calorific value is only 1170KJ/kg, and its calorific value of dried municipal sludge can reach 15MJ/kg, the storage that the mud after heated drying can be stable, sells as product.
At present, the dry technology of high-moisture brown coal, coal slime, mud is divided into dehydration by evaporation technology and non-evaporating dehydrolysis technology conventionally.In dehydration by evaporation, removing of water is by directly or indirectly the heat that is equivalent to water evaporation latent heat being added on wet stock, and water is removed with the form of gaseous state; In non-evaporating dehydrolysis process, water does not undergo phase transition, and directly with liquid form, removes.Because moisture evaporation needs amount of heat, therefore traditional dry run is a high energy consumption process.
The economy and the security that how to improve high-moisture brown coal, coal slime and drying sludge, reduce dry run energy consumption effectively, improves power plant efficiency and will become problem demanding prompt solution.
Publication number is that the Chinese patent literature of CN101907383B discloses belt-conveying drying system and the method for utilizing solar energy to realize brown coal dehydration upgrading, comprise the feeding preheating chamber, drier and the discharged material cooling chamber that by belt-type conveying equipment, are connected successively, drier is divided into air preheating chamber and two parts of hothouse by a vertical partition, on partition, establish through hole, air preheating chamber is established wind entrance, hothouse is established wind outlet; Described discharged material cooling chamber is established new wind entrance, the wind outlet of discharged material cooling chamber connects the wind entrance of air preheating chamber by airduct, the wind outlet of hothouse is connected to the wind entrance of feeding preheating chamber and the wind entrance of air preheating chamber by airduct simultaneously, and the wind outlet of feeding preheating chamber is connected to coal dust piece-rate system.But owing to adopting individual layer treating apparatus, the treatment effeciency of material is lower, and equipment occupation space is larger.
Summary of the invention
The invention provides a kind of simple in structure, rational Multi-layer belt type drying system is set, by reclaim using waste heat from tail gas and utilize dry after the higher upgrading material of temperature heat medium is heated, reduced the energy consumption of dry run.This drying system, for the dry processing before transporting containing wet stock as brown coal, coal slime or mud etc., can be realized to efficient, clean utilization to material.
A system, comprises that top transmits guipure with the drying box of exhaust outlet and the multilayer that is positioned at drying box, and the input that lower floor transmits guipure is accepted the output of the adjacent transmission guipure in upper strata, and every layer is transmitted guipure below and is provided with some circulating fans;
In described drying box, be provided with and be divided into hothouse and the upper and lower two-part horizontal baffle of cooling chamber;
Described cooling chamber bottom is provided with air outlet, and inside is provided with the air-introduced machine for air draft, and described air outlet and air-introduced machine are located at the both sides of transmitting guipure;
In described hothouse, be provided with heater, the air inlet of heater is communicated with the air outlet of air-introduced machine, and heater is provided with a plurality of and interior guipure air outlet one to one that transmits of hothouse;
As preferably, in described hothouse, transmit guipure at least two-layer, in cooling chamber, transmission guipure is one deck at least.Through the dry and cooling processing of multilayer, material can obtain fully and uniformly dry.
Described transmission guipure is made by the stainless sheet steel of boring a hole, and by motor, through gearbox, is driven, and transmits guipure and can carry out speed governing by motor.Adjacent transport network interband, mesh scavenging machine is equipped with at the revolution position of lower floor's transmission guipure and upper strata transmission guipure, to remove the material particles sticking on mesh.
In described hothouse, transmit the speed of service of guipure and controlled through material bed resistance drop by air, by adjusting, transmit the speed of service of guipure and can control the distribution of heat medium again.As preferably, in described hothouse, undermost transport network tape speed is lower, makes bed of material thickening, can make most of air stream two-layer thinner material bed through what start, to improve total drying efficiency.
As preferably, the distribution density of circulating fan is every 2.5～4m
2transport network band area arranges a circulating fan.The distribution of circulating fan is gathered and is controlled in above-mentioned scope, can guarantee to transmit guipure take up an official post meaning section material abundant heat exchange and take into account economical and energy-conservation.
As preferably, described heater is fin steam heater, and the heat transfer property of fin steam heater is good and resistance is little.Heat medium reaches 135 ℃ of left and right after heating, and the superheated steam amount that this temperature is flowed through in fin steam heater is controlled, and to guarantee the security of heat transfer process, wherein, the chart that superheated steam amount can utilize empirical data to draw accurately calculates.
As preferably, described Multi-layer belt type drying system also comprises the heat exchanger of being located at outside drying box, and described heat exchanger is divided into inner and outer tubes, and drying medium is in the circulation of heat exchanger inner tube, and band waste heat tail gas circulates through heat exchanger outer tube.The air outlet of described heat exchanger inner tube is communicated with the air outlet of cooling chamber, and the air inlet of heat exchanger outer tube is communicated with the exhaust outlet of drying box by exhaust duct.
As preferably, described exhaust outlet is at least two, and each exhaust outlet place is equipped with wet-emitting blower, and all exhaust outlets gather to exhaust duct.
As preferably, described exhaust duct is provided with deduster.
As preferably, described drying box top and bottom are respectively equipped with charging aperture and discharging opening.
As preferably, the dry and cooling procedure of material is all carried out in airtight drying box, can effectively prevent the lignitoid spontaneous combustion of Partial Species material, and dry run dust can not leak, and has improved security and the feature of environmental protection of dry run.
Technological process of the present invention is as follows:
Heat medium of the present invention is air, through fragmentation, the charging aperture by drying box top enters on the transmission guipure in hothouse the wet stocks such as high-moisture brown coal, coal slime or mud, directly contact with the air of dry heating indoor, carry out convection heat transfer' heat-transfer by convection, mass transfer exchange, obtain the high temperature upgrading material after drying and dehydrating; High temperature upgrading material is transported to cooling chamber by transmitting guipure, directly contacts with the air after preheating in cooling chamber, after cooling, from the discharging opening of drying box bottom, draws off.Air in cooling chamber after preheating after contact with high temperature upgrading material by secondary preheating, in air-introduced machine introducing heater; The tail gas that the band producing in hothouse has surplus heat is discharged from exhaust outlet, passes into heat exchanger, for the preheating of fresh air after dehumidifying, dedusting.
Compared with prior art, tool of the present invention has the following advantages:
Multi-layer belt type drying system in the present invention is simple in structure, easy for installation, adopts layered arrangement, and treating capacity is large, and floor space is little, and equipment is compacter; Flexible operation, every layer of transport network tape speed can carry out independent control, can control each layer of material thickness according to drying regime, guarantee hot-air cross-flow drying wet stock, and material is in the discharging and fill process of upper and lower two-layer transmission guipure, the stacking of storeroom becomes loosening, and specific area increases, and the total productive capacity of dryer group is improved;
Native system reduces the energy consumption of dry materials process by reclaiming using waste heat from tail gas, after recycling is dry, the higher upgrading material of temperature heats heat medium, reduces further the energy consumption of dry run.
Native system is the transportation pre-treatment containing wet stock for high-moisture brown coal, coal slime, mud etc., can improve low heat valve, reduce cost of transportation; For the preposition of electricity generation system, be dried, can improve unit generation efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of Multi-layer belt type drying system of the present invention:
In figure: 1-charging aperture, 2-exhaust outlet, 3-exhaust duct, 4-wet-emitting blower, 5-drying box, 6-hothouse, 7-fin steam heater, 8-air outlet, 9-air-introduced machine, 10-cooling chamber, 11-discharging opening, 12-transmits guipure, 13-circulating fan, 14-horizontal baffle, 15-air outlet, 16-pressure fan, 17-ajutage, 18-air cleaner, 19-heat exchanger, 20-deduster.
The specific embodiment
Referring to Fig. 1, a kind of Multi-layer belt type drying system, comprise that top is with the drying box 5 of two exhaust outlets 2 and five layers of transmission guipure 12 of being made by the stainless sheet steel of boring a hole being positioned at drying box 5, the input of lower floor's transmission guipure is accepted the output of the adjacent transmission guipure in upper strata, every layer of transmission guipure below is provided with some circulating fans 13, and the distribution density of circulating fan 13 is every 2.5～4m
2transport network band area arranges one.
Multi-layer belt type drying system also comprises:
Drying box top and bottom are respectively equipped with charging aperture 1 and discharging opening 11, be provided with and be divided into hothouse 6 and the upper and lower two-part horizontal baffle 14 of cooling chamber 10 in drying box;
In cooling chamber, be provided with upper and lower two-layer transmission guipure, wherein, on the sidewall of cooling chamber left side, the position of corresponding lower floor transmission guipure is provided with air outlet 15, and air-introduced machine 9 is positioned at the right side that guipure is transmitted on upper strata.
In hothouse, be provided with three layers and transmit guipure, transmit guipure right side and be provided with a fin steam heater 7, the bottom of this heater is provided with air inlet, is communicated with the air outlet of air-introduced machine 9, and heater left side has three and transmits guipure position air outlet 8 one to one with three layers;
The part of ajutage 17 before entering heat exchanger 19 connects pressure fan 16, between ajutage 17 and pressure fan 16, is provided with again air cleaner 18; The part of exhaust duct 3 before entering heat exchanger 19 is provided with deduster 20.
Air in environment is in pressure fan is drawn into ajutage, after filtering, air cleaner enters heat exchanger inner tube, preheating in heat exchanger, by ajutage, from the air outlet of cooling chamber bottom, enter in drying box, under the suction force effect of circulating fan, the air after preheating is the directed material that passes through from bottom to top again, because this material is the high temperature upgrading material after hothouse inner drying, temperature is higher, and air absorbs the heat of material when by material, obtains secondary preheating; In the fin steam heater of air after secondary preheating in air-introduced machine enters hothouse, after heating, from three air outlets of fin steam heater, discharge respectively, air after heating transmits the material on guipure by this layer from bottom to top respectively under the effect of each layer of circulating fan, by the object of conducting heat, mass transfer exchange reaches dried material.The tail gas producing after dry is discharged in exhaust outlet, then passes in heat exchanger after wet-emitting blower hydrofuge, deduster dedusting, and the waste heat of tail gas is used for carrying out heat exchange with fresh air, preheat fresh air, and the tail gas after heat exchange directly enters in environment.
Material is inputted drying box from charging aperture after fragmentation, evenly be laid on the transmission guipure of the hothouse the superiors, transmitting under the drive of guipure, by whole hothouse, with hothouse in the heat transfer, mass transfer exchange process of hot-air, temperature of charge raises, moisture content removes.Dried material enters in cooling chamber, contacts heat exchange occurs with the air of preheating in cooling chamber, and material is cooled, and has completed the drying and dehydrating of material and cooling whole process.
Claims (8)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310548774.3A CN103575077B (en) | 2013-11-07 | 2013-11-07 | A kind of Multi-layer belt type drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310548774.3A CN103575077B (en) | 2013-11-07 | 2013-11-07 | A kind of Multi-layer belt type drying system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103575077A true CN103575077A (en) | 2014-02-12 |
| CN103575077B CN103575077B (en) | 2015-09-16 |
Family
ID=50047387
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310548774.3A Active CN103575077B (en) | 2013-11-07 | 2013-11-07 | A kind of Multi-layer belt type drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103575077B (en) |
Cited By (34)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104566431A (en) * | 2014-12-16 | 2015-04-29 | 华北电力大学 | Low-temperature drying and coal conveying integrated equipment for raw coal |
| CN104896899A (en) * | 2015-06-19 | 2015-09-09 | 江西伊卡斯特科技有限公司 | Belt drier for preparing solid phosphoric acid catalyst and drying method |
| CN104990388A (en) * | 2015-08-10 | 2015-10-21 | 秦朝东 | Efficient rice drying machine |
| CN104990393A (en) * | 2015-08-14 | 2015-10-21 | 吉首大学 | Mesh turning plate type drying machine utilizing exhaust heat |
| CN105004162A (en) * | 2015-08-14 | 2015-10-28 | 吉首大学 | Waste heat recovery type steam plate-press dryer |
| CN105066628A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat recovery screen hole plate turnover type dryer |
| CN105066632A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat utilization type steam flat dryer |
| CN105066626A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat utilization screen hole plate turnover type dryer |
| CN105066627A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat recovery screen mesh plate turning type drying machine |
| CN105174683A (en) * | 2015-10-22 | 2015-12-23 | 得利满水处理系统(北京)有限公司 | Sludge reduction combined treatment system and method |
| CN105180620A (en) * | 2015-08-14 | 2015-12-23 | 吉首大学 | Tail heat recovery type steam flat-plate dryer |
| CN105271628A (en) * | 2015-10-22 | 2016-01-27 | 得利满水处理系统(北京)有限公司 | Low-temperature drying system and method of sludge |
| CN105333713A (en) * | 2015-11-23 | 2016-02-17 | 浙江联鑫板材科技有限公司 | Galvanized piece drying device |
| WO2016062256A1 (en) * | 2014-10-24 | 2016-04-28 | 中盈长江国际新能源投资有限公司 | Method and apparatus for using excess heat from power plant flue gas to dry biomass fuel |
| CN106322968A (en) * | 2016-08-31 | 2017-01-11 | 四川中测量仪科技有限公司 | Gas drying machine used for tea making |
| CN106766802A (en) * | 2017-01-20 | 2017-05-31 | 梁平县奇爽食品有限公司 | Tunnel drier |
| CN106931757A (en) * | 2017-03-25 | 2017-07-07 | 天津市食新食异食品有限公司 | Peanut drying equipment |
| CN107144095A (en) * | 2017-03-16 | 2017-09-08 | 太仓澄天机械有限公司 | A kind of Full automatic drying box |
| CN107388796A (en) * | 2017-09-12 | 2017-11-24 | 无锡市强力干燥设备厂 | Multilayer conveyor type dryer |
| CN107956075A (en) * | 2016-10-14 | 2018-04-24 | 无锡市信谊机械有限公司 | A kind of multiple field textile evaporates dry integrated machine |
| CN109198371A (en) * | 2017-07-07 | 2019-01-15 | 江苏自然爱食品有限公司 | A kind of wheaten food drying device |
| CN109556381A (en) * | 2018-12-21 | 2019-04-02 | 贺州学院 | Calcium carbonate net belt type drier |
| CN110260607A (en) * | 2019-06-18 | 2019-09-20 | 山东琦泉能源科技有限公司 | A kind of box-type drying device |
| CN110715534A (en) * | 2019-11-11 | 2020-01-21 | 江西农业大学 | Automatic wet circulating infrared hot air drying device of accuse |
| CN110881679A (en) * | 2018-09-11 | 2020-03-17 | 秦皇岛烟草机械有限责任公司 | Multistage belt tobacco drying equipment |
| CN111153584A (en) * | 2020-03-03 | 2020-05-15 | 江苏釜鼎干燥工程有限公司 | Two-stage method heat recycling sludge drying system and drying method thereof |
| CN112062441A (en) * | 2020-09-16 | 2020-12-11 | 中国科学院广州能源研究所 | Energy-saving sludge drying system and sludge drying method |
| CN112254495A (en) * | 2020-11-20 | 2021-01-22 | 上海蓁实信息科技咨询中心 | Multi-layer energy-saving drying device |
| CN112389969A (en) * | 2020-10-13 | 2021-02-23 | 洪木兰 | Folding layered conveying device with sorting function for coal mine |
| CN113294974A (en) * | 2021-06-25 | 2021-08-24 | 景津环保股份有限公司 | Closed type drying machine |
| CN113371968A (en) * | 2020-11-24 | 2021-09-10 | 湖南清源智造设备有限公司 | Medium-temperature heat pump sludge drying device and sludge drying method |
| CN113776314A (en) * | 2021-11-11 | 2021-12-10 | 中建环能科技股份有限公司 | Heat exchange device |
| CN114777457A (en) * | 2021-06-20 | 2022-07-22 | 威海汇创企业管理咨询有限公司 | Thermal cracking carbon black granulation drying-machine |
| CN116734572A (en) * | 2023-07-20 | 2023-09-12 | 河南羚锐制药股份有限公司 | Low-power consumption vacuum drying device |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107642951B (en) * | 2016-07-28 | 2019-09-17 | 中国科学院理化技术研究所 | A hybrid heat pump drying system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101034006B1 (en) * | 2010-07-20 | 2011-05-11 | 리턴에너지 주식회사 | White lead and environmental pollutant removal and energy recovery dryer |
| CN202135654U (en) * | 2011-02-28 | 2012-02-08 | 四川中测量仪科技有限公司 | Tea leaf drier |
| CN202532841U (en) * | 2012-03-26 | 2012-11-14 | 江苏牧羊集团有限公司 | Drying-cooling all-in-one machine |
| CN203561164U (en) * | 2013-11-07 | 2014-04-23 | 浙江大学 | A multi-layer belt drying system |
-
2013
- 2013-11-07 CN CN201310548774.3A patent/CN103575077B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101034006B1 (en) * | 2010-07-20 | 2011-05-11 | 리턴에너지 주식회사 | White lead and environmental pollutant removal and energy recovery dryer |
| CN202135654U (en) * | 2011-02-28 | 2012-02-08 | 四川中测量仪科技有限公司 | Tea leaf drier |
| CN202532841U (en) * | 2012-03-26 | 2012-11-14 | 江苏牧羊集团有限公司 | Drying-cooling all-in-one machine |
| CN203561164U (en) * | 2013-11-07 | 2014-04-23 | 浙江大学 | A multi-layer belt drying system |
Non-Patent Citations (1)
| Title |
|---|
| 金国淼等: "《干燥设备》", 31 August 2002, article "厢式和带式干燥器设计", pages: 67-70 * |
Cited By (45)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101946741B1 (en) | 2014-10-24 | 2019-05-20 | 종잉 창지앙 인터내셔널 뉴 에너지 인베스트먼트 컴퍼니 리미티드 | Method and apparatus for using excess heat from power plant flue gas to dry biomass fuel |
| KR20170072320A (en) * | 2014-10-24 | 2017-06-26 | 종잉 창지앙 인터내셔널 뉴 에너지 인베스트먼트 컴퍼니 리미티드 | Method and apparatus for using excess heat from power plant flue gas to dry biomass fuel |
| WO2016062256A1 (en) * | 2014-10-24 | 2016-04-28 | 中盈长江国际新能源投资有限公司 | Method and apparatus for using excess heat from power plant flue gas to dry biomass fuel |
| RU2666839C1 (en) * | 2014-10-24 | 2018-09-12 | Чжунин Чанцзян Интернэшнл Нью Энерджи Инвестмент Ко., Лтд. | Method and device for using excess heat from flue gas of a power plant for drying fuel from biomass |
| CN104566431A (en) * | 2014-12-16 | 2015-04-29 | 华北电力大学 | Low-temperature drying and coal conveying integrated equipment for raw coal |
| CN104896899A (en) * | 2015-06-19 | 2015-09-09 | 江西伊卡斯特科技有限公司 | Belt drier for preparing solid phosphoric acid catalyst and drying method |
| CN104896899B (en) * | 2015-06-19 | 2017-09-15 | 彤程化学（中国）有限公司 | A kind of band drier and drying means prepared for solid phosphoric acid catalyst |
| CN104990388A (en) * | 2015-08-10 | 2015-10-21 | 秦朝东 | Efficient rice drying machine |
| CN104990388B (en) * | 2015-08-10 | 2018-04-27 | 盐城迈克瑞机械有限公司 | A kind of high-efficiency rice drying machine |
| CN105004162A (en) * | 2015-08-14 | 2015-10-28 | 吉首大学 | Waste heat recovery type steam plate-press dryer |
| CN105180620A (en) * | 2015-08-14 | 2015-12-23 | 吉首大学 | Tail heat recovery type steam flat-plate dryer |
| CN105066627A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat recovery screen mesh plate turning type drying machine |
| CN105066626A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat utilization screen hole plate turnover type dryer |
| CN105066632A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat utilization type steam flat dryer |
| CN105180620B (en) * | 2015-08-14 | 2018-07-24 | 青岛成策节能机械有限公司 | A kind of tail heat recovery steam plate-press dryer |
| CN105066628A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat recovery screen hole plate turnover type dryer |
| CN104990393A (en) * | 2015-08-14 | 2015-10-21 | 吉首大学 | Mesh turning plate type drying machine utilizing exhaust heat |
| CN105004162B (en) * | 2015-08-14 | 2018-04-06 | 吉首大学 | Tail heat recovery steam plate-press dryer |
| CN104990393B (en) * | 2015-08-14 | 2017-09-19 | 和县伊迈炭业有限责任公司 | A kind of tail heat utilization sieve aperture turnover plate type drying machine |
| CN105271628A (en) * | 2015-10-22 | 2016-01-27 | 得利满水处理系统(北京)有限公司 | Low-temperature drying system and method of sludge |
| CN105174683A (en) * | 2015-10-22 | 2015-12-23 | 得利满水处理系统(北京)有限公司 | Sludge reduction combined treatment system and method |
| CN105333713A (en) * | 2015-11-23 | 2016-02-17 | 浙江联鑫板材科技有限公司 | Galvanized piece drying device |
| CN106322968A (en) * | 2016-08-31 | 2017-01-11 | 四川中测量仪科技有限公司 | Gas drying machine used for tea making |
| CN107956075A (en) * | 2016-10-14 | 2018-04-24 | 无锡市信谊机械有限公司 | A kind of multiple field textile evaporates dry integrated machine |
| CN107956075B (en) * | 2016-10-14 | 2020-07-03 | 无锡市信谊机械有限公司 | Multilayer formula fabrics rapid steamer drying all-in-one |
| CN106766802A (en) * | 2017-01-20 | 2017-05-31 | 梁平县奇爽食品有限公司 | Tunnel drier |
| CN107144095A (en) * | 2017-03-16 | 2017-09-08 | 太仓澄天机械有限公司 | A kind of Full automatic drying box |
| CN106931757A (en) * | 2017-03-25 | 2017-07-07 | 天津市食新食异食品有限公司 | Peanut drying equipment |
| CN109198371A (en) * | 2017-07-07 | 2019-01-15 | 江苏自然爱食品有限公司 | A kind of wheaten food drying device |
| CN107388796A (en) * | 2017-09-12 | 2017-11-24 | 无锡市强力干燥设备厂 | Multilayer conveyor type dryer |
| CN110881679A (en) * | 2018-09-11 | 2020-03-17 | 秦皇岛烟草机械有限责任公司 | Multistage belt tobacco drying equipment |
| CN109556381A (en) * | 2018-12-21 | 2019-04-02 | 贺州学院 | Calcium carbonate net belt type drier |
| CN110260607A (en) * | 2019-06-18 | 2019-09-20 | 山东琦泉能源科技有限公司 | A kind of box-type drying device |
| CN110715534A (en) * | 2019-11-11 | 2020-01-21 | 江西农业大学 | Automatic wet circulating infrared hot air drying device of accuse |
| CN111153584A (en) * | 2020-03-03 | 2020-05-15 | 江苏釜鼎干燥工程有限公司 | Two-stage method heat recycling sludge drying system and drying method thereof |
| CN112062441A (en) * | 2020-09-16 | 2020-12-11 | 中国科学院广州能源研究所 | Energy-saving sludge drying system and sludge drying method |
| CN112062441B (en) * | 2020-09-16 | 2024-11-05 | 中国科学院广州能源研究所 | Energy-saving sludge drying system and sludge drying method |
| CN112389969A (en) * | 2020-10-13 | 2021-02-23 | 洪木兰 | Folding layered conveying device with sorting function for coal mine |
| CN112254495A (en) * | 2020-11-20 | 2021-01-22 | 上海蓁实信息科技咨询中心 | Multi-layer energy-saving drying device |
| CN113371968A (en) * | 2020-11-24 | 2021-09-10 | 湖南清源智造设备有限公司 | Medium-temperature heat pump sludge drying device and sludge drying method |
| CN114777457A (en) * | 2021-06-20 | 2022-07-22 | 威海汇创企业管理咨询有限公司 | Thermal cracking carbon black granulation drying-machine |
| CN113294974A (en) * | 2021-06-25 | 2021-08-24 | 景津环保股份有限公司 | Closed type drying machine |
| CN113776314A (en) * | 2021-11-11 | 2021-12-10 | 中建环能科技股份有限公司 | Heat exchange device |
| CN116734572A (en) * | 2023-07-20 | 2023-09-12 | 河南羚锐制药股份有限公司 | Low-power consumption vacuum drying device |
| CN116734572B (en) * | 2023-07-20 | 2024-01-02 | 河南羚锐制药股份有限公司 | Low-power consumption vacuum drying device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103575077B (en) | 2015-09-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103575077A (en) | Multi-layer belt type drying system | |
| CN203561164U (en) | A multi-layer belt drying system | |
| CN212222781U (en) | System for utilize flue gas or steam waste heat to carry out airtight stoving to mud | |
| CN102954678B (en) | Utilize method and the device thereof of biomass boiler flue gas drying biomass material | |
| CN101907383B (en) | Belt-conveying drying system and method for realizing dehydration and upgrading of lignite by using solar energy | |
| CN210773189U (en) | MVR vacuum tube bundle drying system with waste steam conversion device | |
| CN106242233A (en) | low temperature sludge drying system | |
| CN110671907A (en) | MVR vacuum tube bundle drying system with waste steam conversion device | |
| CN211645030U (en) | Sludge closed heat pump drying equipment | |
| CN201844667U (en) | Belt type conveying and drying system and device using solar energy to dehydrate and improve quality of brown coal | |
| CN102797064A (en) | Drying and adjusting process and device for viscose fibers | |
| CN203586725U (en) | Fermented forage drying device | |
| CN101929095A (en) | Air supplying and exhausting system for dryer hood of paper machine | |
| CN103575082A (en) | Fermented feed drying system | |
| CN105466171A (en) | Vacuum tube bundle drying system with waste heat for pneumatic drying | |
| CN110772938B (en) | Intensive smoke plume treatment and purification system and method | |
| CN208187026U (en) | A kind of sludge dehumidification type multistage recuperation of heat anhydration system | |
| CN104126660B (en) | A kind of round-the-clock fluidized bed process crop dryer | |
| CN209537262U (en) | A kind of pump type heat divides warm area drying system | |
| CN206385016U (en) | A kind of sludge at low temperature highly effective drying equipment | |
| CN216694207U (en) | Fluidized bed type solid waste drying system utilizing industrial waste heat | |
| CN203653403U (en) | Dyeing sludge drying equipment | |
| CN216716928U (en) | Energy-saving grain drier | |
| CN213873439U (en) | Waste heat utilization device of freezing type dryer | |
| CN104710094A (en) | Printing and dyeing sludge drying method and apparatus thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |